Bhawna Chugh1, Ashish K Singh2, Sanjeeve Thakur1, Balaram Pani3, Hassane Lgaz4, Ill-Min Chung4, Ranjana Jha5, Eno E Ebenso6. 1. Department of Chemistry, Netaji Subhas Institute of Technology, University of Delhi, New Delhi 110078, India. 2. Department of Applied Science, Bharati Vidyapeeth's College of Engineering, New Delhi 110063, India. 3. Department of Chemistry, Bhaskaracharya College of Applied Science, University of Delhi, New Delhi 110078, India. 4. Department of Crop Science, College of Sanghur Life Science, Konkuk University, Seoul 05029, South Korea. 5. Department of Physics, Netaji Subhas Institute of Technology, University of Delhi, New Delhi 110078, India. 6. Department of Chemistry, School of Mathematical and Physical Sciences, Faculty of Agriculture, Science and Technology, North-West University, Mafikeng Campus, Private Bag X2046, Mmabatho 2735, South Africa.
Abstract
In the present study, comparative analyses of corrosion inhibition property of few thiadiazole-derived bis-Schiff bases for mild steel in 1 M HCl were done. Various electrochemical experiments (electrochemical impedance spectroscopy and potentiodynamic polarization), as well as weight loss experiments, were employed to study the anticorrosion activity of bis-Schiff bases as inhibitors. The highest inhibition efficiency was obtained at an optimum concentration of 125 ppm for all inhibitors. Potentiodynamic polarization studies explain the mixed type but predominantly the cathodic nature of all inhibitors. The Langmuir adsorption isotherm was used to describe the mechanism of adsorption. The change in the value of activation energy on the addition of inhibitors reflects the mixed mode of interaction between the inhibitor and metallic surface. Scanning electron microscopy with energy-dispersive spectroscopy, X-ray diffraction, and X-ray photoelectron spectroscopy analyses confirmed the adsorption of bis-Schiff bases on the metal surface and thereby shielding from corrosion. Besides, the relevance between inhibition efficiency and the molecular structure of an inhibitor was theoretically examined via quantum chemical calculations and molecular dynamics simulations. All the results show consistent agreement with each other.
In the present study, comparative analyses of corrosion inhibition property of few thiadiazole-derived bis-Schiff bases for mild steel in 1 M HCl were done. Various electrochemical experiments (electrochemical impedance spectroscopy and potentiodynamic polarization), as well as weight loss experiments, were employed to study the anticorrosion activity of bis-Schiff bases as inhibitors. The highest inhibition efficiency was obtained at an optimum concentration of 125 ppm for all inhibitors. Potentiodynamic polarization studies explain the mixed type but predominantly the cathodic nature of all inhibitors. The Langmuir adsorption isotherm was used to describe the mechanism of adsorption. The change in the value of activation energy on the addition of inhibitors reflects the mixed mode of interaction between the inhibitor and metallic surface. Scanning electron microscopy with energy-dispersive spectroscopy, X-ray diffraction, and X-ray photoelectron spectroscopy analyses confirmed the adsorption of bis-Schiff bases on the metal surface and thereby shielding from corrosion. Besides, the relevance between inhibition efficiency and the molecular structure of an inhibitor was theoretically examined via quantum chemical calculations and molecular dynamics simulations. All the results show consistent agreement with each other.
Corrosion
protection of metallic structures has attracted significant interest
due to immense financial and safety misfortunes as a result of corrosion
in various industries. Various industries utilize mild steel as an
imperative construction material as it is extensively used and has
diverse applications, thanks to its low price and exceptional physical
and mechanical properties.[1−5] However, in spite of its compelling use, mild steel employed in
industries is easily vulnerable to corrosion, particularly in acidic
media. Consequently, owing to low resistance to corrosion, it is necessary
to discover certain methods to safeguard mild steel from corrosion.
Among various available methods, one of the widely used strategies
is employing organiccompounds as corrosion inhibitors for mitigating
corrosion in acidic solutions.[6−9] Several heterocycliccompounds containing heteroatoms
(N, S, and O-atoms), π-bonds, and aromatic systems exhibit excellent
anticorrosion performance.[10,11] Organiccompounds of
such a kind are easily adsorbed on the mild steel surface owing to
the bonding of lone pairs and/or π-electrons with the metal
surface, subsequently diminishing the corrosion.[12,13] Recently, Schiff bases (−N=CH), resulting from the
reaction of aldehyde and amines, as proficient corrosion inhibitors
have acquired a substantial amount of interest by the researchers.[14−18] Inhibitors having both nitrogen and sulfur are profoundly efficient
for corrosion inhibition in contrast with those containing either
nitrogen or sulfur.[19] Thiadiazoles are
one of such class of compounds containing both nitrogen and sulfur
whose Schiff bases have been reported and impacts of such compounds
on corrosion inhibition have been examined.[20,21] In addition to this, thiadiazole derivatives also possess antimicrobial
properties.[22,23] Noncytotoxic property of thiadiazole
derivatives makes them environmental friendly inhibitors.[24,25] In continuation of the research on advancement of thiadiazolecompounds
as effective corrosion inhibitors in acidic media, the current work
discusses the inhibitive performance of four thiadiazole bis-Schiff
base derivatives, namely, N,N′-(1,4-phenylenebis(methanylylidene))bis(5-(methylthio)-1,3,4-thiadiazol-2-amine)
(PMTTA), 5,5′-((1,4-phenylenebis(methanylylidene))bis(azanylylidene))bis(1,3,4-thiadiazole-2-thiol)
(PATT), N,N′-(1,4-phenylenebis(methanylylidene))bis(5-methyl-1,3,4-thiadizol-2-amine)
(PMTA), and N,N′-(1,4-phenylenebis(methanylylidene))bis(1,3,4-thiadiazol-2-amine)
(PTA) on corrosion of mild steel in 1 M HCl by employing a weight
loss technique, potentiodynamic polarization, electrochemical impedance
spectroscopy (EIS), scanning electron microscopy (SEM), atomic force
microscopy (AFM), X-ray diffraction (XRD), and modern surface characterization
such as X-ray photoelectron spectroscopy (XPS). In addition to these,
attenuated total reflectance (ATR) is performed to understand the
adsorption of inhibitors by interacting with the mild steel. The effect
of change in temperature in different electrolytic solutions of inhibitors
is studied and different thermodynamic and kinetic parameters are
also determined. All the experimental findings are correlated with
the theoretical data using density functional theory (DFT), Fukui
indices, and molecular dynamics (MD) simulations to describe the mechanism
of effective coordination of the inhibitor with the surface of mild
steel.
Result and Discussion
Synthesis
Chemical structures of the synthesized inhibitors were proved by
Fourier transform infrared (FT-IR) and 1HNMR. The 1HNMR spectra of all the synthesized compounds are given in Figures S1–S4. The 1HNMR and
FT-IR spectral data for all inhibitors are presented as below:
Effect of Substituent and Inhibitor’s Concentration
All the four synthesized inhibitors, that is, PATT, PMTA, PMTTA,
and PTA are found highly efficient for the corrosion inhibition of
mild steel. On varying the concentration of the inhibitor used, change
in the rate of corrosion and hence inhibition efficiency was observed
as shown in Table . The weight loss measurements were done at 308 K. On increasing
the concentration of the inhibitor, the corrosion rate declined and
thus, inhibition ameliorated which is shown in Figure a. This illustrates that on increasing the
concentration, inhibitor molecules are basically adsorbed on the metallic
surface to the greater extent by providing a wider surface coverage.
Consequently, the interaction between metal and acid solution is restricted.
The effect of the substituent of the thiadiazole ring on corrosion
was analyzed, and it was found to follow the trend as PMTTA > PATT
> PMTA > PTA. Thus, the best inhibition performance was shown
by PMTTA at 125 ppm, and EWL % was determined
as 92.6%. The superior inhibition efficiency of PMTTA might be due
to the introduction of electron-donating functional groups like methylsulfanyl
which increase the performance of inhibitor molecules to transfer
electrons to the vacant d-orbitals of Fe, thus retarding the corrosion
process, as it is well known that the efficiency of inhibitor molecule
increases with its electron donating power capacity.[26] In any case, an additional increment in the concentration
of the inhibitor affords no recognizable modification of inhibition
efficiency which could be seen from Table and Figure a. This might be due to the saturation of the surface.
Hence, 125 ppm is chosen as the optimum concentration.
Table 1
Corrosion Parameters Obtained from Weight Loss Measurements
for Mild Steel in 1 M HCl with Various Concentrations of PMTTA, PATT,
PMTA, and PTA
inhibitor
concentration of inhibitor (ppm)
weight loss in triplicate (mg)
mean
weight loss (mg)
standard deviation (σ)
EWL % (mean value)
corrosion rate (mm y–1)
1 M HCl
121.4
122.1
122.5
122.0
0.39
90.41
PMTTA
10
28.7
29.1
29.2
29.0
0.18
76.2
21.49
25
16.7
16.8
17.2
16.9
0.18
86.1
12.52
50
13.6
14.2
14.2
14.0
0.24
88.5
10.38
100
9.7
9.8
9.9
9.8
0.07
91.9
7.26
125
8.8
9.0
9.2
9.0
0.14
92.6
6.67
150
8.8
8.8
9.1
8.9
0.12
92.7
6.60
175
8.6
8.7
9.1
8.8
0.18
92.7
6.52
PATT
10
36.1
37.2
37.4
36.9
0.49
69.7
27.35
25
22.5
22.8
23.7
23.0
0.44
81.1
17.05
50
15.8
15.9
16.0
15.9
0.07
87.0
11.78
100
11.6
11.9
11.9
11.8
0.12
90.3
8.74
125
10.8
10.9
11.3
11.0
0.18
90.9
8.15
150
10.6
10.8
11.3
10.9
0.25
91.0
8.08
175
10.6
10.9
10.9
10.8
0.12
91.1
8.00
PMTA
10
58.9
59.0
59.1
59.0
0.07
51.6
43.72
25
47.5
47.9
48.0
47.8
0.18
60.8
35.42
50
34.5
34.8
35.4
34.9
0.32
71.3
25.86
100
22.7
22.9
23.1
22.9
0.14
81.2
16.97
125
14.8
14.9
15.3
15.0
0.18
87.7
11.12
150
14.6
14.8
15.3
14.9
0.25
87.7
11.04
175
14.7
14.7
15.0
14.8
0.12
87.8
10.97
PTA
10
56.5
56.8
57.1
56.8
0.21
53.4
42.09
25
52.5
53.0
53.2
52.9
0.25
56.6
39.20
50
35.8
35.9
36.3
36.0
0.18
70.5
26.68
100
30.8
30.8
31.1
30.9
0.12
74.6
22.90
125
23.0
24.3
24.7
24.0
0.62
80.3
17.79
150
23.5
23.9
24.3
23.9
0.28
80.4
17.71
175
23.5
23.6
24.0
23.7
0.18
80.5
17.56
Figure 1
(a) Variation of inhibition
efficiency with the concentration of various inhibitors, (b) Arrhenius
plot of log CR vs 1/T, (c) plot of log CR/T vs 1/T, and (d) Langmuir adsorption isotherm plots
for all the synthesized inhibitors.
(a) Variation of inhibition
efficiency with the concentration of various inhibitors, (b) Arrhenius
plot of log CR vs 1/T, (c) plot of log CR/T vs 1/T, and (d) Langmuir adsorption isotherm plots
for all the synthesized inhibitors.
Calculation of Thermodynamic and Activation Parameters
Arrhenius and transition state equations have been employed to express
the dependency of the corrosion rate on temperature. This is illustrated
using the following equationswhere Ea represents activation
energy, λ is the pre-exponential factor, R is
the universal gas constant, ΔH* is enthalpy
of activation, and ΔS* is entropy of activation.A straight line is observed from the plot of log CR and 1/T having slope (−Ea/2.303R) and intercept log
λ, as depicted in Figure b. Thus, using slope and intercept of the plot, energy of
activation Ea and pre-exponential factor
λ were calculated. The estimated activation energies for the
all the inhibited solutions was found to be greater in comparison
to the solution with bare acid, as summarized in Table . Higher the value of activation
energy, Eacorresponds to increase in
the energy barrier for the corrosion phenomenon.[27,28] As a result, inhibition efficiency is increased in the case of inhibited
systems.
Table 2
Activation and Thermodynamic Parameters
for Mild Steel Corrosion in 1 M HCl in the Absence and Presence of
125 ppm Concentration of Inhibitors PMTA, PMTTA, PTA, and PATT
inhibitor
Ea (kJ mol–1)
λ (mg cm–2)
ΔH* (kJ mol–1)
ΔS* (kJ mol–1 K–1)
Kads (M × 104)
–ΔGads° (kJ mol–1)
1 M HCl
32.8
3.74 × 107
30.15
–108.95
PTA
40.3
1.14 × 108
37.64
–99.69
3.33
37.0
PMTA
45.9
7.32 × 108
43.29
–84.22
2.50
36.2
PATT
49.3
1.62 × 109
46.59
–77.65
10.0
39.8
PMTTA
51.3
3.13 × 109
48.66
–72.15
11.1
40.0
In accordance with eq , it could be visualized that the
corrosion rate is dependent on both Ea and λ. In most of the cases, the effect of Ea is more as compared to λ, or in other words, Ea factor dominates over λ to determine
the mild steelcorrosion inhibition phenomenon. It is known that higher Ea and lower λ leads to a decreased corrosion
rate.[6] In the current case, values of both Ea and λ are increasing in order PTA <
PMTA < PATT < PMTTA. Also, Table depicts the order of corrosion rate as PTA > PMTA
> PATT > PMTTA, which implies Ea as a primary decisive factor for the corrosion phenomenon of mild
steel in 1 M HCl. An advantageous physical or chemical interaction
is indicated by upward or downward change of free energy of activation.[19,29] In the present study, though the value of Ea increased for inhibited solution compared to that of bare
acid solution but the change is not so large to consider the interaction
as pure electrostatic or physical. Thus, in the present case, a mixed
mode of interaction (though it is predominantly physical) is involved
between the inhibitor and metal surface.Similarly, with the
help of slope and intercept of the graph log CR/T and 1/T (presented as Figure c), enthalpy and
entropy of activation are evaluated and also summarized in Table . Positive values
of enthalpy of activation (ΔH*) indicated the
endothermic behavior, resulting in a slow process of mild steel dissolution.[30,31]On correlating the values of the entropy of activation (ΔS*) depicted in Table , it is apparent that values of the entropy of activation
increased in the presence of inhibitors than in the absence of inhibitors.
The increment in ΔS* suggests the increase
in disordering on going from the reactant to the activated complex
which means randomness is increased. The adsorption of the organic
substrate from the acidic solution on the mild steel is basically
a quasi-substitution process among the organiccompound in the aqueous
phase and water molecules present at the mild steel surface. As a
result, the adsorption of the organic inhibitor was accompanied by
desorption of water molecules from the mild steel surface. Because
of this phenomenon, an increase in entropy of activation was observed
which might be due to an increase in solvent entropy.[32]
Adsorption Isotherm
On the basis of adsorption of inhibitors on the metallic surface,
a massive amount of information is presented by means of different
adsorption isotherms. Among all adsorption isotherms, Langmuir adsorption
isotherm was accounted to be the most acceptable to justify the adsorption
of all inhibitors on the surface of mild steel on the grounds that
the linear regression coefficient is observed very closest to unity.[33] Langmuir adsorption isotherm is well explained
by the following equationThis relation basically briefs the
dependency of the concentration of inhibitor (Cinh) with the surface coverage (θ) of the inhibitor on
the surface of metals. The percentage surface coverage is defined
as the fraction of the surface covered by an inhibitor molecule and
can be calculated as per eq .The graph of Cinh/θ versus Cinh (Figure d) obtained
at 308 K gives straight lines, and hence, adsorption of inhibitors
comply Langmuir adsorption isotherm more accurately as compared to
other isotherms. Kads signifies affinity
among the adsorbent and adsorbate. Higher values of Kads inferred greater adsorption and subsequently way better
inhibition efficiency.[3]Kads can be ascertained using the intercepts of the straight
lines, which are summarized in Table .Equation represents the relation between the Gibbs free energy of
adsorption and equilibrium constant of adsorption.where R is gas constant, T is absolute temperature, and Kads represents the equilibrium constant of an adsorption–desorption
process.The negative value of Gibbs free energy of adsorption
(ΔGads°) signifies spontaneity of the process;
that is the inhibitor molecules are effectively adsorbed on the surface
of mild steel.[34] It can be seen that the
electrostatic interaction and hence physisorption of the inhibitor
molecule to the metal surface is characterized by ΔGads° ≤
−20 kJ mol–1. However, a highly negative
value of free energy of adsorption (>40 kJ mol–1) signifies a co-ordinate type of bond, that is, chemisorption.[9] In this case, ΔGads° values
are calculated as −37, −36.2, −39.8, and −40
kJ mol–1 for PTA, PMTA, PATT, and PMTTA, respectively,
as given in Table . This suggests that the mechanism involves both physisorption and
chemisorption, that is, mixed mode of interaction.
FT-IR Analysis
FT-IR analysis has been performed for
the identification and confirmation of different functional groups
present in the synthesized compounds. Graphs depicting all the peaks
are given in Figure . It could be seen from the graphs that peak at 1625, 1607, 1619,
and 1604 cm–1 for PTA, PATT, PMTA, and PMTTA, respectively,
confirmed the presence of C=NH (imine group) in the synthesized
compounds, thereby confirming the product formation. The FT-IR spectrum
was also recorded in the ATR mode and represented in Figure . All the characteristic peaks
obtained for the inhibitors were found to shift to the lower frequency
which confirms the interaction between various functional groups present
in the inhibitor and Fe2+.
Figure 2
FT-IR spectra of pure synthesized compounds
(a) PMTTA, (b) PATT, (c) PMTA, and (d) PTA and their film deposited
on the surface of mild steel.
FT-IR spectra of pure synthesized compounds
(a) PMTTA, (b) PATT, (c) PMTA, and (d) PTA and their film deposited
on the surface of mild steel.
Electrochemical Techniques
Potentiodynamic
Polarization Studies
Figure a–d demonstrates the potentiodynamic polarization
plots for all the inhibitors, that is, PMTA, PMTTA, PTA, and PATT
in 1 M HCl solution. Extrapolation was done for cathodic and anodic
lines and the corresponding intersection results in various polarization
parameters, that is, corrosion current density (icorr), corrosion potential (Ecorr), anodic slope (βa), and cathodic slope (βc), which are given in Table . It can be inferred from the data that icorr values are suppressed on increasing the concentration
of inhibitors. This indicated that the inhibitors are strongly adsorbed
on the surface of mild steel, thereby enhancing the corrosion inhibition.
Also, the trend for inhibition efficiency follows the same order,
that is, PMTTA > PATT > PMTA > PTA as interpreted from the
weight loss study. The literature describes that if the variation
in the value of Ecorr is greater than
85 mV with reference to the value obtained with the blank acid solution,
then the inhibitor is said to be a cathodic or anodic inhibitor while
if the difference in the Ecorr value is
less than 85 mV, and it is termed as a mixed type inhibitor.[35] In our current work, it could be seen that the Ecorr shift for all the described inhibitors
with respect to 1 M HCl is less than 85 mV, indicating the mixed type
but predominantly cathodic behavior for all described inhibitors.
The data of Table reflects that a more pronounced change in the value of βc than that of βa, which suggests predominantly
the cathodic nature of inhibitors. This mixed type but predominantly
cathodic nature of the inhibitors may be due to effective adsorption
of the protonated inhibitor molecule on the cathode.
Figure 3
Potentiodynamic polarization
curves of mild steel in 1 M HCl with various concentrations of (a)
PMTTA, (b) PATT (c) PMTA, and (d) PTA.
Table 3
Tafel Polarization Parameters for Mild Steel in the
Absence and Presence of Different Concentrations of PMTA, PMTTA, PTA,
and PATT in 1 M HCl
inhibitor
concentration (ppm)
–Ecorr (mV vs SCE)
icorr (μA cm–2)
βa (mV dec–1)
βc (mV dec–1)
EPDP % (mean value)
standard
deviation (σa)
CR (mm y–1)
1 M HCl
445
3165.4
104.1
174.3
1.52
37.20
PMTTA
10
480
803.3
98.8
195.2
74.6
1.00
9.42
25
477
502.3
91.3
188.4
84.1
0.84
5.89
50
476
466.5
79.3
185.2
85.3
1.18
5.47
100
485
411.0
102.7
188.7
87.0
0.82
4.82
125
482
302.1
97.8
170.2
90.4
1.25
3.54
PATT
10
490
1497.0
119.8
151.4
52.7
1.70
17.57
25
478
1113.0
107.4
183.4
64.8
1.61
13.06
50
482
919.2
85.7
182.5
71.0
0.94
10.78
100
481
553.6
107.3
272.2
82.5
1.35
6.49
125
492
373.6
113.1
184.6
88.2
1.00
4.38
PMTA
10
477
1763.7
117.1
158.4
44.3
0.50
20.70
25
492
1522.7
126.5
160.9
51.9
0.68
17.87
50
461
1217.2
120.8
198.6
61.5
1.61
14.28
100
455
687.9
95.2
169.4
78.3
0.70
8.07
125
481
553.6
107.3
272.2
82.5
0.45
6.49
PTA
10
489
2017.1
120.6
172.6
36.3
0.30
23.67
25
488
1755.3
122.5
166.9
44.5
0.90
20.60
50
465
1195.1
119.0
246.6
62.2
1.18
14.02
100
480
1035.9
117.5
199.0
67.3
1.59
12.15
125
482
705.3
90.2
196.2
77.7
1.85
8.27
Calculated from corrosion current density.
Potentiodynamic polarization
curves of mild steel in 1 M HCl with various concentrations of (a)
PMTTA, (b) PATT (c) PMTA, and (d) PTA.Calculated from corrosion current density.
Electrochemical
Impedance Spectroscopy
Nyquist plots for mild steel immersed
in 1 M HCl solution with and without inhibitors are presented in Figure a–d. All the
impedance parameters, obtained after fitting the equivalent circuit
to the experimental data, are shown as Table .
Figure 4
Nyquist plots of mild steel in 1 M HCl in the
absence and presence of different concentrations of (a) PMTTA, (b)
PATT (c) PMTA, and (d) PTA and (e) equivalent circuit used to fit
the experimental data.
Table 4
Electrochemical
Impedance Parameters for Mild Steel in the Absence and Presence of
Different Concentrations of PMTA, PMTTA, PTA, and PATT in 1 M HCl
name of inhibitor
conc. of
inhibitor (ppm)
Rs (Ω cm2)
Rct (Ω cm2)
RL (Ω cm2)
L (H)
Q (μF·s(n–1))
n
Cdl (μF cm–2)
EEIS (%)
1 M HCl
0.430
2.40
0.8
10.3
719.2
0.801
157.1
PMTTA
10
0.858
18.16
2.6
7.8
185.3
0.852
68.91
86.8
25
0.686
25.03
3.3
7.2
150.6
0.863
62.1
90.4
50
0.623
34.80
3.1
6.5
124.5
0.868
54.4
93.1
100
0.759
42.60
4.7
5.5
100.8
0.871
44.9
95.0
125
0.507
47.80
4.9
4.2
90.9
0.874
41.5
94.9
PMTA
10
0.613
6.2
1.6
8.9
302.1
0.831
84.2
61.3
25
1.421
8.8
2.5
8.0
260.4
0.837
79.7
72.7
50
0.704
10.0
2.6
7.4
231.6
0.839
72.3
76.0
100
0.660
15.9
2.7
6.4
200.9
0.840
67.3
84.9
125
0.996
18.8
2.8
5.7
175.6
0.842
60.1
87.3
PATT
10
0.514
8.70
2.2
8.1
202.1
0.846
63.7
72.4
25
0.490
11.50
2.3
7.7
176.2
0.855
61.6
79.1
50
0.760
18.30
2.9
6.2
145.6
0.859
55.1
86.9
100
0.501
34.80
3.1
5.8
125.1
0.860
51.7
93.1
125
0.588
46.00
3.8
4.4
104.6
0.863
44.8
94.8
PTA
10
0.608
3.70
0.6
9.6
423.2
0.815
97.7
35.2
25
0.478
7.3
0.7
8.8
315.3
0.819
82.4
67.1
50
0.613
8.5
0.7
8.1
279.4
0.822
75.5
71.8
100
0.662
9.6
0.9
7.0
248.2
0.829
71.4
75.0
125
0.554
12.2
1.2
5.9
221.8
0.835
68.9
80.3
Nyquist plots of mild steel in 1 M HCl in the
absence and presence of different concentrations of (a) PMTTA, (b)
PATT (c) PMTA, and (d) PTA and (e) equivalent circuit used to fit
the experimental data.The impedance behavior
of mild steel in HCl solution in the absence and with inhibitors,
PATT, PTA, PMTA, and PMTTA, was controlled by the combined effect
of resistance, capacitance, and inductance. However, the occurrence
of a major portion of the Nyquist plot in positive Y-axis emphasized that the resistance and capacitance of the system
controlled its impedance behavior. This is due to the occurrence of
the electrical double layer or development of oxide layer at the MS–acid
solution interface. The shape of Nyquist plots is depressed semicircles
instead of perfect semicircle. The depression is associated with roughness
and inhomogeniety of the metal surface.[36] The Nyquist plots obtained in this study consists of two loops;
one capacitive loop at higher frequency followed by a low-frequency
inductive loop. The appearance of inductive loops at lower frequency
might be due to more effective adsorption of inhibitors or due to
the relaxation process obtained by the adsorption of Clads– and Hads+ on the surface
of the electrode. However, the size of inductive loops increased regularly
with increasing concentration of inhibitors which indicates readsorption
of the inhibitor over the MS surface.Considering it, double
layer capacitance (Cdl) in the circuit
was substituted by a constant phase element (CPE) in the equivalent
circuit to obtain more accurate and optimized fit. The equivalent
circuit employed for fitting all the experimental results is depicted
in Figure e.The impedance (ZCPE) can be estimated
by the following equationwhere Q represents the magnitude of CPE, j is an
imaginary number (j2 = −1), ω is angular frequency,
and n is the phase exponent which represents the degree of irregularity.Angular frequency (ω) is attained from eq described below at the frequency with the
highest imaginary impedance.Double layer capacitance
values are estimated by applying the following relationValue of n is always between 0 and 1 as it justifies
the difference from an ideal behavior. As per the Helmholtz model
depicted in eq , double
layer capacitance is inversely linked to the thickness of the electrical
double layer which acts as a protective layer.where d is the thickness of the double layer, ε
is dielectricconstant, ε0 is vacuum permittivity,
and A is an area of the electrode.So it is
apparent from the data in Table that on increasing the concentration of inhibitors,
a gradual decrease in the value of Cdl is observed (68.9–41.5 for PMTTA; 84.2 to 60.1 for PMTA;
63.7 to 44.8 for PATT; and 97.7 to 68.9 for PTA), which reflects a
lowering in local dielectricconstant or/and enlargement in the thickness
of the double layer.[37] This implies that
the addition of the studied inhibitors led to the reduction in Cdl values which might be due to the substitution
of water molecules by inhibitor molecules at the electrode surface.
As a consequence of which, an increment in surface coverage of mild
steel by the inhibitor molecules was observed which increased the
efficiency of an inhibitor. Also, the decrease in Cdl leads to a decrease in active area (A), as stated in eq that indeed supports the effectiveness of the inhibitors in providing
a surface film that inhibits the anodic dissolution of the metal.Further, it could be illustrated from the curves that on the addition
of the inhibitor, the impedance behavior of mild steel is substantially
altered and diameter of the semicircle obtained in the Nyquist plots
is enlarged subsequently in the presence of inhibitors. The low solution
resistance with all the inhibitor indicated that inhibitor’s
solution had no impact on the impedance behavior especially in the
high-frequency region.Bodes-phase angle plots in the absence
and with all the four inhibitors are represented in Figure a–d. The phase angle
curves exhibit single maxima at an intermediate frequency range which
signifies one time constant. This could be seen from the graphs that
in the case of inhibited solutions, phase angles are somewhat higher
as compared to 1 M HCl solution, leading to increased surface smoothness
of the mild steel with all inhibitors. More negative values of the
phase angle leads to more capacitive behavior which means there is
more adsorption of inhibitors on the surface and thus more will be
the surface smoothness. Furthermore, broadening of the curves is observed
which confirms the accumulation of the molecule of inhibitors on the
surface of mild steel. Also, the effect gets more pronounced on increasing
the concentration of inhibitors.[28] Now,
considering all the factors, on comparing all the inhibitors, PMTTA
was found to be most efficient with a maximum inhibition efficiency
of 94.6% at 125 ppm concentration. The order of EEIS % was attained as PMTTA > PATT > PMTA > PTA.
Figure 5
(a–d)
Bode-phase angle plots of mild steel in 1 M HCl in absence and presence
of different concentrations of all inhibitors.
(a–d)
Bode-phase angle plots of mild steel in 1 M HCl in absence and presence
of different concentrations of all inhibitors.
Surface Characterization
SEM–EDX
Figure a–f presents the SEM images of the surface of
mild steel in 1 M HCl solution with and without optimum concentration
of the inhibitors. The Figure a represents the mild steel surface before immersion in acid
solution. The mild steel surface got damaged when exposed to bare
acid solution, as shown by Figure b. On the contrary, the mild steel surface remained
intact appreciably by the presence of inhibitors (Figure c–f), indicating suppression
in the corrosion phenomenon. This finding followed the other experimental
results. The smoother texture of mild steel samples exposed to inhibited
acid solutions (Figure c–f) compared to that which is exposed to bare acid solution
(Figure b) indicated
that the mild steel surfaces were prevented by the attack of an aggressive
solution by the presence of inhibitors.
Figure 6
SEM images of mild steel
for (a) MS surface before immersion in 1 M HCl, (b) after immersion
in 1 M HCl, (c) after immersion in 1 M HCl +125 ppm of PMTTA, (d)
after immersion in 1 M HCl + 125 ppm of PATT, (e) after immersion
in 1 M HCl + 125 ppm of PMTA, and (f) after immersion in 1 M HCl +
125 ppm of PTA.
SEM images of mild steel
for (a) MS surface before immersion in 1 M HCl, (b) after immersion
in 1 M HCl, (c) after immersion in 1 M HCl +125 ppm of PMTTA, (d)
after immersion in 1 M HCl + 125 ppm of PATT, (e) after immersion
in 1 M HCl + 125 ppm of PMTA, and (f) after immersion in 1 M HCl +
125 ppm of PTA.The formation of the protective
film due to adsorption of inhibitors on the surface of mild steel
is further confirmed by scanning their energy-dispersive spectroscopy
(EDX) spectra. The EDX plots and elemental composition are shown in Figure a–f. It could
be seen that EDX spectra of mild steel in blank HClconstitutes peak
only for iron and carbon. However, new additional peaks are obtained
in the EDX spectra in the presence of bis-Schiff bases which are characteristic
of nitrogen and sulfur which confirms the presence of these elements
on the surface of mild steel. This implies the adsorption of bis-Schiff
bases on the surface which inhibits the corrosion. In addition to
this, EDX spectra demonstrate that the percentage composition of iron
subsequently decreases on the addition of bis-Schiff bases which may
be due to surface coverage (Table S1).The
deposition of different elements over the MS surface can be seen as
mapping images provided in Figures S5–S10.
Figure 7
EDX spectra of mild steel for the (a) MS surface before immersion
in 1 M HCl, (b) after immersion in 1 M HCl, (c) after immersion in
1 M HCl + 125 ppm of PMTTA, (d) after immersion in 1 M HCl + 125 ppm
of PATT, (e) after immersion in 1 M HCl + 125 ppm of PMTA, and (f)
after immersion in 1 M HCl + 125 ppm of PTA.
EDX spectra of mild steel for the (a) MS surface before immersion
in 1 M HCl, (b) after immersion in 1 M HCl, (c) after immersion in
1 M HCl + 125 ppm of PMTTA, (d) after immersion in 1 M HCl + 125 ppm
of PATT, (e) after immersion in 1 M HCl + 125 ppm of PMTA, and (f)
after immersion in 1 M HCl + 125 ppm of PTA.
AFM
The topography of the mild steel
samples was analyzed with the help of an atomic force microscope. Figure a–f demonstrates
2-D and 3-D AFM images of mild steel after immersing in different
HCl solutions for 3 h. Also, Figure a–f represents a roughness profile diagram of
mild steel after immersing in different HCl solutions for 3 h.
Figure 8
Atomic force
micrographs of mild steel (a) before immersion in 1 M HCl, (b) after
immersion in 1 M HCl in the absence of an inhibitor, (c) after immersion
in 1 M HCl + 125 ppm PMTTA, (d) after immersion in 1 M HCl + 125 ppm
PATT, (e) after immersion in 1 M HCl + 125 ppm PMTA, and (f) after
immersion in 1 M HCl + 125 ppm PTA.
Figure 9
Surface
roughness profile diagram of mild steel (a) before immersion in 1
M HCl solution, (b) after immersion in 1 M HCl, (c) after immersion
in 1 M HCl + 125 ppm PMTTA, (d) after immersion in 1 M HCl + 125 ppm
PATT, (e) after immersion in 1 M HCl + 125 ppm PMTA, and (f) after
immersion in 1 M HCl + 125 ppm PTA.
Atomic force
micrographs of mild steel (a) before immersion in 1 M HCl, (b) after
immersion in 1 M HCl in the absence of an inhibitor, (c) after immersion
in 1 M HCl + 125 ppm PMTTA, (d) after immersion in 1 M HCl + 125 ppm
PATT, (e) after immersion in 1 M HCl + 125 ppm PMTA, and (f) after
immersion in 1 M HCl + 125 ppm PTA.Surface
roughness profile diagram of mild steel (a) before immersion in 1
M HCl solution, (b) after immersion in 1 M HCl, (c) after immersion
in 1 M HCl + 125 ppm PMTTA, (d) after immersion in 1 M HCl + 125 ppm
PATT, (e) after immersion in 1 M HCl + 125 ppm PMTA, and (f) after
immersion in 1 M HCl + 125 ppm PTA.It is apparent from Figure b that the average roughness of abraded mild steel before
immersion in acid solution was found to be 22.2 nm while the average
roughness of the mild steel sample immersed in 1 M HCl solution reached
the maximum value, that is 1335 nm (Figure b). This infers that mild steelcorroded
by aggressive HCl solution and developed some cracks. However, the
values of average roughness for inhibited solutions were somewhat
reduced in comparison to the uninhibited solution and were found to
follow the order PMTTA < PATT < PMTA < PTA, and the values
obtained were 22.9, 39.3, 69.1, and 291 nm respectively. This may
be due to the adsorption of the inhibitors on the surface of mild
steel which helps in protection from getting corroded. The effect
of an inhibitor on the texture of the surface of mild steelcan be
seen from the roughness profile diagram presented in Figure .
XRD
Analysis
XRD is known to be an excellent technique for material
characterization, identification of crystalline phase, and quantitative
phase analysis. Thus, the XRD method could be utilized for the characterization
of corrosion products obtained after immersion of mild steel in aggressive
HCl solution. The supremacy of the inhibitor, PMTTA leads us to select
it to study its effect on the XRD pattern. Figure depicts the comparison of XRD patterns
of corrosion products formed on the mild steel in 1 M HCl in the absence
and presence of the inhibitor, PMTTA. The XRD pattern for mild steel
immersed in 1 M HCl shows three peaks at 2θ = 44.88, 82.38,
65°. When the XRD pattern of mild steel immersed in inhibited
acid solution (1 M HCl + 125 ppm PMTTA) was scanned, the same three
peaks were observed at 2θ = 44.66, 64.27, and 82.34°. Peaks
at 2θ = 44.66, 44.88, 82.34, and 82.38° are assigned metalliciron (Fe). The peak at 2θ = 64.27 and 65° is characteristic
for oxides of iron such as iron oxy-hydroxide (FeOOH).[38] Thus, it can be observed that the peak due to
FeOOH is present in the presence of an inhibitor but its intensity
is reduced. Also, the increase in the intensity of Fe peaks is observed.
This clearly indicates the protection of the metal surface from corrosion
by forming a protective layer of the inhibitor which resists the formation
of any corrosion products such as oxides of oxy-hydroxides.
Figure 10
XRD patterns
of corrosion products formed on the mild steel in 1 M HCl in the absence
and presence of the inhibitor, PMTTA.
XRD patterns
of corrosion products formed on the mild steel in 1 M HCl in the absence
and presence of the inhibitor, PMTTA.
X-Ray Photoelectron Spectroscopy
The
composition of the film developed by adsorption of different substances
on the mild steel surface was detected by XPS. The XPS spectra of
mild steel were scanned in the absence and presence of the inhibitor,
PMTTA, which is predicted to be a highly efficient compound among
all. The XPS spectrum of mild steel immersed in bare HCl solution
was also obtained in order to compare and confirm the adsorption of
the inhibitor on the surface of mild steel. The XPS spectra in the
absence and presence of PMTTA are presented in Figure a–i. The deconvolution procedure
is used for fitting various peaks in order to assign peak for respective
elements. This could be done by making use of XPS Peak Fit 4.1 software.
Figure 11
XPS
spectra for mild steel immersed in 1 M HCl solution without an inhibitor:
(a) C 1s; (c) Fe 2p; and (e) O 1s and XPS spectra for mild steel immersed
in 1 M HCl solution with the inhibitor, PMTTA: (b) C 1s; (c) Fe 2p;
(f) O 1s; (g) N 1s; and (h) S 2p and (i) a survey scan for both inhibited
as well as the uninhibited solution.
XPS
spectra for mild steel immersed in 1 M HCl solution without an inhibitor:
(a) C 1s; (c) Fe 2p; and (e) O 1s and XPS spectra for mild steel immersed
in 1 M HCl solution with the inhibitor, PMTTA: (b) C 1s; (c) Fe 2p;
(f) O 1s; (g) N 1s; and (h) S 2p and (i) a survey scan for both inhibited
as well as the uninhibited solution.The C 1s spectrum of the uninhibited system shows three peaks at
248.9, 285.1, and 288.4 eV, whereas four peaks, that is, 248.8, 285.2,
286.2, and 288.2 eV are ascribed for the inhibited system as given
in Figure a,b. Peaks
at 248.9, 285.1, 284.8, and 285.2 eV can be due to C–H, C–C,
and C=C and also might be due to the presence of contaminant
hydrocarbons on the surface for uninhibited and inhibited systems,
respectively.[39,40] The peak at 286.2 eV in the PMTTA-inhibited
system is due to the presence of C=N and C–N bond in
imine and thiadiazole species or the C–S bond which confirms
the adsorption of the inhibitor on the mild steel surface.[39,41] The peak at 288.4 and 288.2 eV for uninhibited and inhibited solution,
respectively,[42] might be due to carboncontamination on the surface due to O–C=O.The
XPS spectra of Fe 2p can be deconvoluted into two peaks corresponding
to Fe 2p3/2 and Fe 2p1/2. Fe 2p3/2 shows four peaks, that is, 710.8, 713, 715, and 719.8 eV for blank
1 M HCl, while three peaks for the inhibited system, that is, PMTTA
which are given as 710.8, 713, 715.4 eV. These are presented in Figure c–d. The
peak at 710.8 eV is ascribed as a ferric compoundFe3+ of
Fe2O3 and/or FeO(OH).[39,43] However, Fe2O3 and FeO(OH) were differentiated
from the O 1s XPS spectrum. The peak at 713 eV is ascribed to FeCl3 accumulated on the metal surface.[41] The peak at 715.4 eV in inhibited solution is characteristic of
Fe(II) species.[44] This means there is no
transformation of Fe(II) to Fe(III) in the presence of PMMTA, or in
other words, there is the existence of stable ferrous compounds on
the PMTTA-treated surface. This effectively supports the anti-corrosion
activity of PMTTA as an inhibitor as the inhibitor molecules are coordinated
with ferrous species to form a stable and insoluble PMMTA–Fe(II)complex which retards the corrosion process of mild steel.[45] The peaks appeared at 715 and 719.8 eV for 1
M HCl are attributed to the satellites of Fe(II) and Fe(III), respectively.[46] Similarly, Fe 2p1/2 can be deconvoluted
into two peaks, that is, 724.4 and 725.9 eV for an uninhibited solution
while one peak is obtained at 724.4 eV for an inhibited solution.
These peaks are also represented to Fe3+ species, that
is, Fe2O3 and FeO(OH).[47] In addition, the intensity of Fe peaks is somewhat lower in the
case of an inhibited system as compared to the uninhibited system.The XPS spectrum of O 1s consists of three peaks for blank 1 M
HCl while two peaks in the case of an inhibited system, as presented
in Figure e,f. The
peaks located at 530 and 530.1 eV can be attributed as the peak of
O2– of ferric oxidesFe2O3 or/and Fe3O4, which means the oxygen atom
that is coordinated to the Fe atom in oxides, respectively, for uninhibited
and inhibited solutions.[43,47,48] Other peaks located at 531.6 and 531.5 eV are interpreted as OH– of hydrous iron oxidesFeO(OH) which usually appears
at 531.7 ± 0.2 eV.[49] The latter peak
at 529.9 eV in uninhibited, that is, blank 1 M HCl is ascribed to
oxygen atoms of absorbed water molecules. However, this peak is absent
in the case of the inhibited solution. This means that the absorbed
water molecules present on the surface are being replaced by the inhibitor
molecules.[48]The high-resolution
N 1s XPS spectrum can be deconvoluted into two peaks at 399.3 and
400.1 eV, as displayed in Figure g. The first peak at around 399.3 eV is representative
of the unprotonated C–N and −C=N bond which is
present itself in the inhibitor.[39,50] On the other
hand, the second peak at 400.1 eV is basically ascribed to the N–Fe
bond which arises due to coordination of nitrogen in the inhibitor
complex with Fe on the steel surface.[39]The XPS spectrum for S 2p can be deconvoluted into three peaks
located at 161.8, 163.7, and 168.5 eV, as presented in Figure h. The first peak centered
on 161.8 eV might be due to disulfide species, that is, FeS2. The peak centered on 163.7 eV is attributed to neutral sulfur (−S)
in the inhibitor. The third peak at 168.5 eV is ascribed to sulfurcoordinated to Fe to form the S–Fecomplex and/or it can also
be due to sulfur atoms which are in a more positive environment.[41]In addition to this, a survey scan for
both inhibited as well as the uninhibited solution is presented in Figure i, which represents
all the elements presents on the surface of mild steel. The data drawn
from XPS analysis for blank 1 M HCl and PMTTAsteel surface gives
direct evidence of adsorption of the PMTTA inhibitor on the mild steel
surface.
DFT Calculations
Global Reactivity Descriptors
Quantum chemical calculations
offer unprecedented and precise information into the geometric and
electronic structure of newly synthesized corrosion inhibitors.[55] Herein, DFT calculations using the hybrid functional
B3LYP, generalized gradient approximated (GGA), and meta-GGA functionals
are conducted to investigate global and local reactivity descriptors
of four corrosion inhibitors. Optimized geometry and Frontier molecular
orbital’s density distribution obtained using meta-GGA are
depicted in Figure . Some of the quantum chemical parameters are shown in Table .
Figure 12
Optimized molecular
structures and Frontier molecule orbital density distributions of
investigated compounds obtained using m-GGA functional.
Table 5
Computed Quantum Chemical Parameters for the Four
Inhibitor Molecules Using B3LYB, GGA, and mGGA Functionals
methods
inhibitors
EHOMO (eV)
ELUMO (eV)
ΔEgap (eV)
ΔN110
GGA
PMTTA
–5.307
–3.566
1.741
0.22
PTA
–5.854
–3.665
2.189
0.027
PATT
–5.482
–3.647
1.835
0.139
PMTA
–5.698
–3.47
2.228
0.105
mGGA
PMTTA
–5.723
–3.691
2.032
0.05
PTA
–6.787
–3.259
3.528
–0.057
PATT
–5.855
–3.782
2.073
0.0007
PMTA
–6.13
–3.513
2.617
–0.0005
B3LYB
PMTTA
–6.381
–3.125
3.256
0.02
PTA
–6.786
–3.261
3.525
–0.057
PATT
–6.411
–3.263
3.148
–0.005
PMTA
–6.806
–3.053
3.753
–0.029
Optimized molecular
structures and Frontier molecule orbital density distributions of
investigated compounds obtained using m-GGA functional.The assumption is that a corrosion inhibitor with
a relatively flat (or planar) orientation can cover a large surface
area when binding to a metal surface.[56] On the other hand, functional groups are very recognized by their
ability to increase the interactive force of an inhibitor molecule.[57] From the results, we can get valuable conclusions
for the geometry of each inhibitor molecule. We can see that the molecular
structure of PTA and PATTcompounds seem to be more planar than others,
that is, PMTA and PMTTA. The introduction of methyl and sulfanyl groups
at both thiadiazole nuclei alters the planarity of PMTA and PMTTA
while an unobvious effect was observed in the case of the thiol group.
In the case of the highest occupied molecular orbital (HOMO) and lowest
unoccupied molecular orbital (LUMO) distribution, we can observe that
the isodensity in HOMO and LUMO of all compounds is equally distributed
throughout the entire molecular structure of inhibitors. Particularly,
in the case of PMTTA, the LUMO orbital is more concentrated on the
phenyl and its linked (sulfanyl) thiadiazole while the HOMO orbital
is mainly dispersed on the other (sulfanyl) thiadiazole. The distribution
of HOMO and LUMO orbitals in all compounds is very similar to each
other. This could lead to further increased adsorption of inhibitors
on the metal surface through dual interactions, that is, interactions
between the unshared electron pair of heteroatoms and vacant d-orbitals
of iron atoms. Unpaired electrons are attracted to the metal surface,
which makes them more reactive.The calculated quantum chemical
parameters, that is, the highest occupied molecular orbital energy
(EHOMO), lowest unoccupied molecular orbital
energy (ELUMO), the energy gap (ΔEgap = ELUMO – EHOMO), and the number of transferred electrons
(ΔN) are given in Table . The HOMO energy corresponds to the ionization
potential and thus represents the propensity of an inhibitor molecule
to share an electron.[58] Higher HOMO energy
potentially leads to a higher electron donating tendency, whereas
the LUMO energy corresponds to the electron affinity and it is a measure
of the electron transport level.[59] Lower
LUMO energy means a higher electron-accepting tendency of an inhibitor
molecule. The donor–acceptor interactions can also be measured
by the number of transferred electrons from the corrosion inhibitors
to the metal surface. A positive ΔN value means
the ability of an inhibitor molecule to share its electrons and vice-versa
for a negative value, and it usually follows the HOMO energy order.[60] According to published studies,[59,61] the energy gap (ΔE) is the primary key factor
predicting chemical reactivity and stability of inhibitor molecules.
As the value of ΔE is decreased, an inhibitor
molecule becomes more reactive. The data in Table suggests that the effect of LUMO energy
to predict the inhibition efficiency was inaccurate in all conducted
methods. In contrast, except in B3LYB results, the trend of EHOMO is PMTTA > PATT > PMTA > PTA,
which agrees with the inhibition efficiency order. The same trend
can be observed from ΔN values. These outcomes
showed that the ability of inhibitor molecules to donate electrons
was improved by introducing electron-donating functional groups like
methyl and sulfanyl, which explains the superior inhibition efficiency
of PMTTA. From Table , we also noticed that the trend for the ΔE values obtained from GGA and B3LYB results failed to agree with
that from experimental results while the results from mGGA show a
good agreement. Unsurprisingly, these outcomes show that the reactivity
of inhibitor molecules increases as the electron-donating power increases.
However, despite their importance, these data are, in some cases,
insufficient to provide a full understanding of factors controlling
inhibitor’s effectiveness and fail to provide a precise correlation.
Next, we investigated the local reactivity of our compounds using
Fukui functions and got some useful insights.
Local Reactivity: Fukui Functions
Besides global reactivity
descriptors, which might be helpful for the prediction of reactive
parts in inhibitor molecules, actually, Fukui functions and dual descriptor
indices provide a useful tool for the prediction of local reactive
sites and are used as a key analysis tool in identifying potential
atoms responsible for the inhibitor performance.[62] An atomic site with more positive charges (f+) is favorable for a nucleophile
to attack, while an atomic site having more surface negative charges
(f–) is favorable for an electrophile to attack.[62] The various condensed Fukui functions along with the dual
descriptor of our compounds are calculated by applying Hirshfeld population
analysis, which is depicted in Table S2. To well understand the key factors governing the inhibitor performance,
it is very important to determine the effect of the functional groups
on the reactivity of heteroatoms, which are definitely the main reason
responsible on inhibitor effectiveness. The data in Table S2 indicate that all reactive sites in inhibitor PTA
have almost an equal strength in terms of electrophilic and nucleophilic
power. The addition of functional groups to this compound affects
the reactivity of its reactive sites, and a tendency toward the nucleophilic
or electrophiliccharacter is clearly observed in three-substituted
compounds. This leads to an obvious effect on the interactive force
of each compound and thus its corrosion inhibition performance. The
existing data from the literature show that organiccompounds containing
heteroatoms are considered as promising corrosion inhibitors; thus
heteroatoms have an extraordinary potential to improve the inhibition
efficiency of those compounds.[57] A deeper
analysis of results in Table S2 shows that
PMTTA and PMTA have widespread distribution and substantial values
of f– sites, which reflect the higher ability to donate electrons. This
could explain the superior inhibition performance and the strong interaction
of PMTTA and PMTA with the metal surface compared to other compounds.
If we now consider reactive site distribution in these compounds,
that is, PMTTA and PMTA, we can see that the major difference between
them comes from the presence of S17 and S22 in
PMTTA, which do not exist in PMTA. This leads us to conclude that
the electron-donating sulfanyl groups attached to thiadiazole rings
have a greater effect on inhibition efficiency than methyl groups.
Thus, a better inhibition performance was obtained for this compound
(PMTTA).
MD Simulations
Although powerful in investigating electronic properties of an inhibitor
molecule, quantum chemical parameters are not enough to predict the
trend of the inhibition efficiency of inhibitors with high accuracy.
Therefore, it is imperative to search for a robust method for the
modeling of inhibitor–metal interactions in an environment
that can mimic the real experimental condition.[63,64] The results from MD simulations provide a basis for judging an inhibition
performance of an inhibitor molecule and whether it can effectively
protect a metal surface.[65] Herein, the
interaction of four inhibitor molecules and the Fe(110) surface was
analyzed and their adsorption configuration on the metal surface was
obtained, as shown in Figure . By carefully inspecting the results summarized in Figure , almost all inhibitor
molecules showed a strong binding affinity toward the iron surface
and displayed a nearly flat or parallel disposition to the metal surface.
Further, the outcomes reveal that the four inhibitor molecules exhibited
a similar adsorption profile, and only small deviations from complete
parallel adsorption can be observed. In such a situation, the direct
close contact of the inhibitor molecule with the surface of mild steel
would facilitate its adsorption and help in the formation of a compact
adsorption film. Furthermore, the widely dispersed potential reactive
sites of inhibitor’s molecule could provide a large effective
coverage area and strong interactions. As we have seen in the HOMO
and LUMO orbitals distribution and Fukui function indices, a large
number of potential nucleophilic and electrophilic sites could have
a very strong impact on inhibitor–metal interactions. On the
other hand, the interaction and binding energy (BE) are a significant
criterion to estimate extent of the adsorption with inhibitor molecules.
Higher interaction energy basically indicates better adsorption of
an inhibitor molecule with an iron surface.[66] Interestingly, all inhibitor molecules have strong interaction energy
and its increasing trend follows the experimental results, as shown
in Table . However,
the data in Table clearly show that the PMTTA compound gives the maximum BE (defined
as the inverse value of the interaction energy) during the whole simulation
process. Thus, PMTTA is accepted as the most efficient inhibitor compared
to other inhibitors, and the result is consistent with DFT/mGGA results.
Figure 13
Side
view and top view of equilibrium adsorption configurations of different
inhibitors, PMTTA, PATT, PMTA, and PTA on the Fe (1 1 0) surface obtained
by MD simulations.
Table 6
MD Parameters
for the Four Compounds Adsorbed on the Fe(110) Surface in the Presence
of Solvent Species
simulation models
Einteraction (kJ mol–1)
PMTTA
–758.79
PTA
–497.87
PATT
–691.69
PMTA
–633.13
Side
view and top view of equilibrium adsorption configurations of different
inhibitors, PMTTA, PATT, PMTA, and PTA on the Fe (1 1 0) surface obtained
by MD simulations.As previously mentioned, the presence of an electron-rich moiety
along with π-electron should affect the electronic structure
of an inhibitor molecule and help it to easily expel the water molecules
from the metal surface.[67] It is apparent
from the results achieved from MD simulations were in good consistency
with the results obtained from meta-GGA calculations.
Conclusions
The present research work can be summarized
by the following conclusions:All the synthesized thiadiazole bis-Schiff
base derivatives, that is, PTA, PMTA, PATT, and PMTTA were proven
to be effective corrosion inhibitors for mild steel in 1 M HCl medium.
The inhibition efficiency was found to abide the order PMTTA >
PATT > PMTA > PTA.Potentiodynamic polarization data revealed the mixed type nature
of all the inhibitors. EIS experiments showed that the values of Rct increased and double layer capacitance declined
in the presence of bis-Schiff bases as a result of adsorption of these
on the metal surface.Surface characterization such as SEM–EDX, AFM, and XPS reflected
the protective barrier of inhibitors on the steel surface mitigating
corrosion.All the experimental
findings were in fine consistency with the theoretical studies viz.
DFT, Fukui indices, and MD simulations which effectively explained
the relation of the inhibition efficiency with molecular structures
of inhibitors.
Experimental
Section
Material and Sample Preparation
The
composition of mild steel employed for performing corrosion experiments
is depicted in Table . HCl (37%, Merck India) was used to prepare
1 M HCl solution from double distilled water. Stock solution of all
the inhibitors was prepared in 1 M HCl and ethanol (used in 9:1 ratio)
and then was diluted to prepare various concentrations of inhibitors.
All the weight loss and electrochemical analysis were carried out
in 1 M HCl solution having a distinctive amount, viz. 10, 25, 50,
100, and 125 ppm, of an inhibitor. Prior to each experiment, the surface
of mild steel was polished with emery papers of 200, 400, 600, 1000,
1200, and 1500 grades and was cleaned altogether with distilled water
and acetone.
Table 7
Chemical Composition of Mild Steel
elements
C
Si
P
Mn
S
Ni
Cr
Fe
% wt
0.05
0.009
0.012
0.20
<0.01
0.0025
0.001
remainder
Synthesis of Inhibitors
All the thiadiazole-derived
bis-Schiff bases were synthesized by refluxing terephthaldehyde (0.01
mol) with different derivatives of 2-amino-1,3,4-thiadiazole (0.02
mol), that is, 1:2 molar ratio in ethanol (40 mL) using hydrochloric
acid as a catalyst for 8–10 h, as per scheme shown in Figure . The solid precipitate
thus obtained was filtered and dried. The synthesized compounds were
re-crystallized using ethanol in order to obtain pure compounds.
Figure 14
Scheme
of synthesis of all the four inhibitors.
Scheme
of synthesis of all the four inhibitors.FT-IR analysis was performed
using a Thermo Fisher FT-IR spectrometer for confirmation and identification
of different functional groups present in the synthesized compounds.
In addition, the ATR mode was also recorded in order to identify and
understand the interaction between inhibitor molecules and the metallic
surface.Weight loss
estimations have been carried out using mild steel strips of size
2.5 × 2.0 × 0.025 cm3. Weight loss measurements
were performed in 1 M HCl as per ASTM G1[68] with varied concentration of inhibitors specified above at 308 K.
Weight loss analysis was performed at 308 K as it was chosen parallel
to the room temperature. The strips were suspended into different
solutions in the hanging position in a conical flask using rubber
corks and by ensuring complete immersion of strips in the solution.
After completion of experiments, mild steel strips were weighed accurately.
A digital electronic weighing balance has been used for accurate weighing
measurements of mild steel specimens. All the experiments have been
performed by maintaining constant temperatures with the help of a
digital thermostat (Macwin India Ltd.). Weight loss studies were likewise
performed at various temperatures, that is, 318, 328, and 338 K to
analyze the effect of temperature on the corrosion phenomenon. The
loss of weight of mild steel strips was computed which is basically
the difference of weight before and after immersion in the solution.
All the experiments were performed in triplicate sets to get precise
results, and standard deviations were estimated as given in Table . Inhibition efficiency
(EWL %) and corrosion rate (CR; mm y–1) can be calculated from weight
loss measurement as per eqs and 11 as[29]where w0 represents weight loss of mild steel strip
in 1 M HCl, wi is weight loss of mild
steel bearing various inhibitors, w signifies weight
loss (mg) of mild steel, A is area of mild steel
strip utilized (cm2), t is time (h), and D represents the density of mild steel (g cm–3).Electrochemical
experiments were performed using SP-240 Bio-Logic Instrument with
EC lab software for analyzing the data. A three electrode cell setup
was prepared for electrochemical measurements maintained at 308 K.
A platinum electrode was used as a counter electrode, a saturated
calomel electrode (SCE) as a reference electrode, and mild steel as
the working electrode. Rectangular mild steel strips of size 1.0 ×
1.0 × 7.5 cm3 with only 1 cm2 area exposed
to the electrolyte and the remaining being covered by using commercially
available lacquer were used to carry out all measurements.The
electrochemical setup was allowed to stand for 0.5 h to obtain the
steady open circuit potential (OCP) prior to each and every electrochemical
measurements. Potentiodynamic polarization data were recorded in the
potential range of ±250 mV with respect to OCP with a scan rate
1 mV s–1. Cathodic and anodiccurves obtained were
extrapolated using Tafel fit to obtain corrosion potential (Ecorr) and corrosion current density (icorr) directly using the software.Using
the values of corrosion current densities, the inhibition efficiency
from potentiodynamic polarization (EPDP %) could be determined using the following equationwhere icorr0 is corrosion
current density for 1 M HCl, that is, in the absence of an inhibitor
while icorri is corrosion current density in the presence
of an inhibitor.Using eq , the value of the corrosion rate (CR) can also be calculated using corrosion current density
aswhere icorr represents corrosion current density in mA cm–2 and equiv wt and d are the equivalent weight and
density of mild steel, respectively.EIS studies were done in
the frequency range of 100 kHz to 0.01 Hz with a sinus amplitude of
20 mV using an AC signal at OCP. EIS parameters were analyzed using
Z Fit in EC Lab software. Further, the inhibition efficiency from
EIS (EEIS %) can be evaluated using charge
transfer resistance as per the following equationwhere Rcti and Rct0 represent charge transfer resistance
in the presence and absence of an inhibitor in the electrolyte solution,
respectively.The surface morphology of mild steel
strips was analyzed by a scanning electron microscope (Hitachi TM3000)
instrument. Also, the elemental detection was carried out by recording
EDX spectra with Oxford SwiftED 3000. The analysis was performed by
using 1 × 1 × 0.025 cm3 mild steel strips which
were immersed in 1 M HCl in the absence and presence of 125 ppm concentration
of all the inhibitors. After 3 h, strips were cleaned with acetone,
then dried, and subsequently used for analysis. SEM examination was
done at an accelerating voltage of 15 kV, and images were obtained
at 2500k× magnification. EDX data was also obtained at 2500k×
magnification at a voltage ≥ 15 kV.
Atomic
Force Microscopy
For AFM characterization, mild steel strips
of sizes 2 × 2.5 × 0.025 cm3 were immersed in
1 M HCl in the absence and presence of 125 ppm concentration of different
inhibitors for 3 h. The strips were thereafter cleaned and finally
subjected for AFM characterization. The atomic force microscope of
Model-Bruker, Dimension ICON with ScanAsyst was utilized to scan the
surface of mild steel in the tapping mode. The images were scanned
in the chosen area of 10 × 10 μm2. Nanoscope
Analysis software 8.2 was used for analyzing the atomic force micrographs
of MS samples.
XRD Analysis
For XRD characterization, mild steel strips were immersed in 1 M
HCl solution in the absence and presence of 125 ppm PMTTA for 3 h.
The surface film formed on mild steel for both uninhibited and inhibited
acid solution was analyzed using a X-ray diffractometer (model: Rigaku
Ultima IV, Ri). The diffraction patterns obtained were recorded in
the 2θ range of 30–90° with a scan rate 5°/min.
X-ray Photoelectron Spectroscopy
X-ray
photoemission spectroscopic (XPS) measurements were achieved in a
multiprobe surface analysis system (Scienta Omicron, Germany) at a
base pressure of 5 × 10–11 Torr. XPS spectra
were recorded via nonmonochromatic Mg Kα (1253.6 eV) radiation
sources. The high-resolution XPS spectra were recorded at a pass energy
of 20 eV for CLs and 5 eV for the valence band spectra. The BE of
the photoemission line and spectrometer work function calibration
was carried out referring Au 4f7/2 emission line and AuFermi level.
Theoretical Studies
Quantum Chemical Calculations
To theoretically understand
the origin of the inhibitor’s effectiveness and to identify
the most influential parameters that may govern the inhibition efficiency,
we carried out multiple quanta chemical calculations. Quantum chemical
parameters and Fukui functions were determined from DMol3 (quantum mechanical code under DFT approximation of a Materials
Studio Software).[69,70] DFT calculations at generalized
gradient first-principles approximation, GGA, using the Perdew, Burke,
and Ernzerhof formalism recognized as PBE, the meta-generalized gradient
approximation (meta-GGA) exchange–correlation density functional
and the Becke’s three-parameter hybrid functional using the
LYP correlation functional (B3LYP) were done to investigate the electronic
properties of tested compounds.[71−74] The COSMO implicit solvent model was utilized for
performing all the calculations.[75] The
ionization energy and the electronic affinity were determined using
the energies of the HOMO and LUMO orbitals and from which, the electronegativity
and the global hardness of the extract molecules were calculated[76]The fraction of transferred electrons (ΔN)
was calculated using the following equation[77]The work function (ϕ) of Fe(110) was mainly accepted
as 4.82 eV, whereas the absolute hardness ηFe of
iron was determined at 0 as I = A for bulk metals.[78,79]The condensed Fukui functions
and the dual descriptor were predicted on the basis of Hirschfield
population analysis and the finite difference approximation as follows[80]In the abovementioned equations, q represents the electronic
population of an atomic site within a molecule in its neutral (N), anionic (N + 1), or cationic (N – 1) state.
MD
Simulations
MD simulations were carried to generate insights
on interactions between inhibitor molecules and the iron surface using
Materials Studio package.[69] The Fe(110)
plane was used as the metallic substrate as a result of its higher
stabilization energy and its extremely packed structure.[81] Two layers were constructed: a solvent layer
with water molecules (491), chlorine, and hydronium ions (9) along
with an inhibitor molecule and the iron substrate layer. Both layers
were collected in one simulation box (24.82 × 24.82 × 35.69
Å3) and optimized by steepest descent and conjugated
gradient algorithms.[82] The COMPASS force
field[83] and the NVT canonical
ensemble were used for all simulations. The simulations were completed
by time step of 1 fs and simulation time of 2000 ps at 303 K, which
is controlled using the Andersen algorithm.[84] The interaction and the binding energies (EBinding = −Einteraction)
were determined when the system attains the equilibrium state by using
the following equation[85]In the above equation, Esurface+solution signifies the total energy of the Fe(110) and solution without an
inhibitor molecule, Einhibitor denotes
the total energy of an inhibitor molecule alone, and Etotal is the total energy of the full system.